CN101298347B - Covalent bond type inorganic organic composite flocculant, preparation process and use thereof - Google Patents

Covalent bond type inorganic organic composite flocculant, preparation process and use thereof Download PDF

Info

Publication number
CN101298347B
CN101298347B CN2008101159908A CN200810115990A CN101298347B CN 101298347 B CN101298347 B CN 101298347B CN 2008101159908 A CN2008101159908 A CN 2008101159908A CN 200810115990 A CN200810115990 A CN 200810115990A CN 101298347 B CN101298347 B CN 101298347B
Authority
CN
China
Prior art keywords
covalent bond
bond type
type inorganic
organic composite
inorganic organic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN2008101159908A
Other languages
Chinese (zh)
Other versions
CN101298347A (en
Inventor
赵华章
彭建雄
孙娟娟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Peking University
Original Assignee
Peking University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Peking University filed Critical Peking University
Priority to CN2008101159908A priority Critical patent/CN101298347B/en
Publication of CN101298347A publication Critical patent/CN101298347A/en
Application granted granted Critical
Publication of CN101298347B publication Critical patent/CN101298347B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention relates to a covalent bond type inorganic/organic compound flocculant, a production technique and an application thereof. The invention adopts Gamma-APDES (gamma-Aminopropylmethyldiethoxysilane) and aluminum chloride solution as the raw materials to produce the covalent bond type inorganic/organic compound flocculant by gradually dripping alkaline. The a covalent bond type inorganic/organic compound flocculant, the production technique and the application thereof have the advantages that the inorganic constituent and the organic constituent in the flocculant are bonded by covalent bond, which has good stability, good turbidity removal and decoloration effect and wider optimal dosing range. The covalent bond type inorganic/organic compound flocculant can be used for the waterpurification and the turbidity removal, decoloration, deoiling and solid-liquid separation during the wastewater treatment.

Description

A kind of covalent bond type inorganic organic composite flocculant, preparation technology and application thereof
Technical field
The invention belongs to the synthesis technical field of polymeric flocculant in the water treatment field, specifically, the present invention relates to a kind of covalent bond type inorganic organic composite flocculant, preparation technology and application thereof.
Background technology
Coagulation process is most widely used general, a most general unit operation technology in the engineering of water treatment.The coagulating treatment effect is directly determining operation condition, final outflow water quality and the cost of follow-up processing flow.The flocculating effect quality depends on flocculation agent to a great extent.Inorganic polymer flocculant and organic polymer coargulator are to use two more class flocculation agents in the current water treatment.The inorganic polymer flocculant price is relatively cheap, but it is low to have a molecular weight, and is poor at water stability, and the dosage height produces shortcomings such as sludge quantity is big.Organic polymer coargulator has that functional group is many, and molecular weight is big, and consumption is few, and settling velocity is fast, and is applied widely, and sludge quantity is few and be easy to advantages such as dehydration; Shortcoming is that price is higher, to removal ability than fine particle, and best dispensing narrow range, not easy to operate etc.Be comprehensive the two advantage, the normal method that adopts substep to add in the water treatment procedure, will be inorganic with the organic polymer coargulator coupling to reach treatment effect preferably.Though this has reached the purpose of having complementary advantages to a certain extent, the consequent is that operating procedure is loaded down with trivial details, and facility investment is big, and use cost is higher relatively etc.Based on this, inorganic organic composite coagulator arises at the historic moment, it not only can reach and add inorganic and the equal even better flocculating effect of organic floculant with substep, and, on the basis of improving processing efficiency, equipment investment cost and cost for wastewater treatment have been reduced because operating procedure has been simplified in disposable dosing.
At present, the compound inorganic flocculating agent and the organic polymer coargulators such as aluminium system, iron system, iron aluminium system, polysilicate of mainly concentrating on of inorganic and organic floculant are as the various combination between chitin, polyacrylamide (PAM), the dimethyl diallyl ammonium chloride (PDMDAAC) etc.As preparing inorganic organic composite coagulator with polymerize aluminum chloride and chitosan among the patent CN1266821A; Prepare inorganic organic composite coagulator with the polymkeric substance of Dicyanodiamide and formaldehyde, poly-sulphur aluminum chloride and poly-sulphur aluminum calcium chloride among the patent CN1393410A; Adopt acrylamide, N among the patent CN1554592A, N-dimethyl diallyl ammonium chloride or (methyl) acrylyl oxy-ethyl-trimethyl salmiac and aluminium hydroxide (ironic hydroxide, magnesium hydroxide, zinc hydroxide) preparation inorganic organic composite coagulator; Then adopt polymeric aluminum and dimethyl diallyl ammonium chloride to prepare inorganic organic composite coagulator among the patent CN1594128A; Raw material is polymerization iron and dimethyl diallyl ammonium chloride among the patent CN1724404A.But in this class composite flocculation agent " compound " of inorganic component and organic constituent, only combine, be difficult to keep the stability of flocculation agent, thereby the application of influence in actual water treatment by coordination or electrostatic interaction loosely.Therefore this class flocculation agent can only be called " composite " strictly speaking, rather than truly " compound ".Should exist the covalent linkage that connects inorganic component and organic constituent in the real compound inorganic organic composite coagulator, i.e. covalent bond type inorganic organic composite flocculant.
Summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art part, and a kind of covalent bond type inorganic organic composite flocculant, preparation technology and application thereof are provided.
The present invention seeks to realize by following measure: (molecular formula is NH for γ-Aminopropylmethyldiethoxysilane, APDES with γ-aminopropyl diethoxymethyl silane in the present invention 2C 3H 6CH 3Si (OC 2H 5) 2) and AlCl 3Solution is raw material, the preparation covalent bond type inorganic organic composite flocculant.Covalent bond type inorganic organic composite flocculant is that inorganic component and organic constituent are compound with covalent linkage, total aluminium concentration 0.05~0.25mol/L, and Si/Al mol ratio 0.1~0.4, basicity 0.5~2.0, the pH value is 3.50~4.50.
Reaction structure formula of the present invention is:
Figure G2008101159908D00021
Water in the reaction formula is from AlCl 3Water in water in the solution and the NaOH solution.Reaction back Al is a kind of polymeric form.
The preparation technology of covalent bond type inorganic organic composite flocculant is with γ-aminopropyl diethoxymethyl silane APDES and AlCl 3After solution mixed, adopting slowly, an alkaline process made covalent bond type inorganic organic composite flocculant.
Concrete preparation technology is as follows, in there-necked flask, presses Si/Al mol ratio 0.1~0.4, quantitatively adds AlCl 3Solution and γ-aminopropyl diethoxymethyl silane mixes the back and stirs fast under room temperature, adopts constant flow pump to drip NaOH solution, NaOH mole number and AlCl 3Ratio be 0.5~2.0, to basicity B=0.5~2.0, after the gained solution left standstill is treated complete reaction, promptly obtain covalent bond type inorganic organic composite flocculant.
The application of covalent bond type inorganic organic composite flocculant is used for turbidity removal, decolouring, de-oiling and the solid-liquid separation of water supply purification, wastewater treatment process.
The present invention compared with prior art has following advantage:
The organic constituent of 1 covalent bond type inorganic organic composite flocculant is the organo-functional group of γ-aminopropyl diethoxymethyl silane, links to each other with the Si atom by C-Si, and inorganic component is an aluminium salt, passes through Al-O-Si key (AlCl behind the aluminium salt hydrolysis 3Al links to each other with the O atom after the hydrolysis) link to each other with the Si atom, realized the compound of inorganic component and organic constituent with the covalent linkage form.
2 covalent bond type inorganic organic composite flocculants have the turbidity removal good decolorizing effect, characteristics such as best dispensing a wider range.
Embodiment
Enumerate 1 embodiment and 2 application examples below, the present invention is further specified, but be not limited thereto.
Example 1:
Covalent bond type inorganic organic composite flocculant, total aluminium concentration 0.2mol/L, the Si/Al mol ratio is 0.4, and basicity B is 2.0, and the pH value is 4.4.
The preparation method is as follows:
Quantitatively add 50mL respectively by predetermined Si/Al mol ratio in there-necked flask, concentration is the AlCl of 1.0mol/L 3The APDES of solution and 4.32mL.Stir fast under room temperature then, adopt constant flow pump slowly to drip 200mL, concentration is the extremely predetermined B value of NaOH solution of 0.5mol/L, i.e. NaOH mole number and AlCl 3Ratio be 2.0, titration time is 3 hours, gained solution left standstill question response fully after, promptly obtain the product that total aluminium concentration is 0.2mol/L.
1 of application example
The coagulation turbidity removal that the covalent bond type inorganic organic composite flocculant product of above example 1 preparation is used for the kaolin muddy water is handled, simultaneously and traditional aluminum salt flocculant---polymerize aluminum chloride (being called for short PAC, basicity 2.0) contrasts.Raw water turbidity is 90NTU, pH value 7.8.Result is listed in the table 1.
The different dosages of table 1 (in Al, mol/L), after covalent bond type inorganic organic composite flocculant example 1 is handled, the coagulation turbidity removal effect of the residual turbidity of water (NTU)
As can be seen from Table 1, the covalent bond type inorganic organic composite flocculant of the inventive method preparation has the turbidity removal effect more excellent than polymerize aluminum chloride.
2 of application example
The coagulation decoloration that the covalent bond type inorganic organic composite flocculant product of above example 1 preparation is used to contain the colored water of humic acid is handled, simultaneously and traditional aluminum salt flocculant---polymerize aluminum chloride (being called for short PAC, basicity 2.0) contrasts.Former colority of water represents that with the 370nm light absorption value its value is 0.250.The pH value is 6.0.Result is listed in the table 2.
The different dosages of table 2 (in Al, mol/L), after covalent bond type inorganic organic composite flocculant example 1 is handled, the coagulate decoloring effect of the residue colourity of water
Figure G2008101159908D00041
As can be seen from Table 2, the covalent bond type inorganic organic composite flocculant of the inventive method preparation has the decolorizing effect more excellent than polymerize aluminum chloride, and the optimal coagulant dose scope is wideer.

Claims (4)

1. a covalent bond type inorganic organic composite flocculant is characterized in that raw material is organic γ-aminopropyl diethoxymethyl silane and inorganic aluminum chloride, and composite flocculation agent is AlCl 3And γ-aminopropyl diethoxymethyl silane is compound with covalent linkage, total aluminium concentration 0.05~0.25mol/L, and Si/Al mol ratio 0.1~0.4, basicity 0.5~2.0, the pH value is 3.50~4.50,
The reaction structure formula is:
Figure F2008101159908C00011
2. by the preparation technology of the described covalent bond type inorganic organic composite flocculant of claim 1, it is characterized in that after γ-aminopropyl diethoxymethyl silane and liquor alumini chloridi mixing, adopting slowly, an alkaline process makes covalent bond type inorganic organic composite flocculant.
3. according to the preparation technology of the described covalent bond type inorganic organic composite flocculant of claim 2, it is characterized in that, press Si/Al mol ratio 0.1~0.4, under room temperature, stir fast after quantitatively getting liquor alumini chloridi and γ-aminopropyl diethoxymethyl silane mixture, adopt constant flow pump to drip NaOH solution, the NaOH mole number is 0.5~2.0 with the ratio of aluminum chloride, to basicity B=0.5~2.0, after the gained solution left standstill is treated complete reaction, promptly obtain covalent bond type inorganic organic composite flocculant.
4. by the application of the described covalent bond type inorganic organic composite flocculant of claim 1, be used for turbidity removal, decolouring, de-oiling and the solid-liquid separation of water supply purification, wastewater treatment process.
CN2008101159908A 2008-07-01 2008-07-01 Covalent bond type inorganic organic composite flocculant, preparation process and use thereof Active CN101298347B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2008101159908A CN101298347B (en) 2008-07-01 2008-07-01 Covalent bond type inorganic organic composite flocculant, preparation process and use thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2008101159908A CN101298347B (en) 2008-07-01 2008-07-01 Covalent bond type inorganic organic composite flocculant, preparation process and use thereof

Publications (2)

Publication Number Publication Date
CN101298347A CN101298347A (en) 2008-11-05
CN101298347B true CN101298347B (en) 2010-06-02

Family

ID=40078330

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2008101159908A Active CN101298347B (en) 2008-07-01 2008-07-01 Covalent bond type inorganic organic composite flocculant, preparation process and use thereof

Country Status (1)

Country Link
CN (1) CN101298347B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102897887A (en) * 2012-11-09 2013-01-30 天津亿利科能源科技发展股份有限公司 Polymer-containing oil-field wastewater treating agent
CN104085972B (en) * 2014-07-22 2015-10-21 北京大学 A kind of denitrogenation flocculation agent and its preparation method and application
CN108083543A (en) * 2017-11-28 2018-05-29 北京大学深圳研究生院 A kind of Dredged bed mud method for treating residual water of built-up flocculant and application built-up flocculant
CN108178262B (en) * 2017-12-28 2021-01-01 陕西省石油化工研究设计院 Inorganic-organic composite polymeric flocculant with high aluminum ion concentration
CN111573802B (en) * 2020-05-08 2023-04-07 南京师范大学 Hydrophobic modified organic/inorganic composite flocculant and preparation method and application thereof
CN113087220A (en) * 2021-04-27 2021-07-09 同济大学 Method for separating macromolecular organic pollutants in percolate concentrated solution by combined flocculation
CN115057508B (en) * 2022-05-10 2023-06-23 同济大学 Preparation method of quartz sand dead-weight flocculant
CN116813046B (en) * 2023-06-30 2024-03-08 青岛水务集团有限公司 Treatment method of landfill leachate concentrated solution
CN116621387B (en) * 2023-06-30 2023-11-14 青岛水务集团有限公司 Concentrated solution full-quantification treatment system and method
CN117699934B (en) * 2024-02-06 2024-05-10 克拉玛依市弘智油田技术服务有限公司 Water purifying agent and preparation method thereof

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3810843A (en) * 1971-05-28 1974-05-14 Gen Electric Silicone-silica compositions

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3810843A (en) * 1971-05-28 1974-05-14 Gen Electric Silicone-silica compositions

Also Published As

Publication number Publication date
CN101298347A (en) 2008-11-05

Similar Documents

Publication Publication Date Title
CN101298347B (en) Covalent bond type inorganic organic composite flocculant, preparation process and use thereof
Zeng et al. Characterization and coagulation performance of a novel inorganic polymer coagulant—Poly-zinc-silicate-sulfate
CN100386267C (en) High efficiency composite flocculant, its preparation method and application
CN104556331B (en) PAC (polyaluminium chloride)-modified sodium alginate inorganic-organic composite flocculant and preparation method thereof
CN106430495B (en) A kind of preparation method of the composite decoloration flocculant for wastewater treatment
CN103342406B (en) Polymeric silicic acid-polyferric sulfate titanium inorganic macromolecular composite flocculant and preparation method and application thereof
CN101885526A (en) Ternary composite type flocculant, preparation and application
CN106630065A (en) Preparation method of polysilicate aluminum-titanium and chitosan composite flocculant
CN101817912B (en) Formula and preparation method of cationic polymer
CN104724809A (en) Ternary copolymerization flocculating agent based on natural macromolecules and preparation method for ternary copolymerization flocculating agent
CN101423275A (en) Method for preparing composite flocculant
CN101921015B (en) Novel inorganic-organic composite macromolecular decolorizing flocculant and preparation method thereof
CN108178262B (en) Inorganic-organic composite polymeric flocculant with high aluminum ion concentration
CN1266822A (en) Polyaluminium chloride and polyacrylamide compounded efficient flocculant and its preparing process
CN101691252A (en) Method for preparing double-acid ferro-aluminum flocculating agent
CN103754999B (en) A kind of preparation method of polyaluminum ferric sulfochloride flocculant
CN105565459B (en) A kind of poly-ferric chloride-paper mill sludge base aminated polymer composite flocculation agent and preparation method thereof
Xu et al. Influences of polysilicic acid in Al13 species on floc properties and membrane fouling in coagulation/ultrafiltration hybrid process
CN103964554B (en) Polyaluminum sulfate titanium-polydimethyldiallylachloride chloride composite coagulant and preparation and application method thereof
EP2661439A2 (en) Phosphoric acid production gypsum filtration flocculant pre-dilution (make down) with post-filtration phosphoric acid
CN102115240B (en) Polyaluminum sulfate-branched poly(dimethyl diallyl ammonium chloride) composite coagulant and preparation method and application method thereof
CN101298346B (en) Polysilicate aluminum sulphate flocculant, preparation process and use thereof
CN107151030A (en) A kind of preparation method and applications for polymerizeing zirconium chloride inorganic polymer coagulant
CN100509867C (en) Preparation method for oxygen-containing nitrolic acid structure polyalcohol inphase opposition emulsions
CN105152294A (en) Preparation method and application of flocculant for treating urban sewage

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Application publication date: 20081105

Assignee: Beijing Ke Yi innovation environment Technology Co., Ltd.

Assignor: Peking University

Contract record no.: 2013990000272

Denomination of invention: Covalent bond type inorganic organic composite flocculant, preparation process and use thereof

Granted publication date: 20100602

License type: Exclusive License

Record date: 20130524

LICC Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model